CN111790437B - Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof - Google Patents

Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof Download PDF

Info

Publication number
CN111790437B
CN111790437B CN202010680588.5A CN202010680588A CN111790437B CN 111790437 B CN111790437 B CN 111790437B CN 202010680588 A CN202010680588 A CN 202010680588A CN 111790437 B CN111790437 B CN 111790437B
Authority
CN
China
Prior art keywords
taurine
catalyst
tantalum
strontium
pentanone
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010680588.5A
Other languages
Chinese (zh)
Other versions
CN111790437A (en
Inventor
杨东元
扈广法
孙育滨
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shaanxi Yanchang Petroleum Group Co Ltd
Original Assignee
Shaanxi Yanchang Petroleum Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shaanxi Yanchang Petroleum Group Co Ltd filed Critical Shaanxi Yanchang Petroleum Group Co Ltd
Priority to CN202010680588.5A priority Critical patent/CN111790437B/en
Publication of CN111790437A publication Critical patent/CN111790437A/en
Application granted granted Critical
Publication of CN111790437B publication Critical patent/CN111790437B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/89Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0203Impregnation the impregnation liquid containing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0213Preparation of the impregnating solution
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/18After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • B01J2229/186After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00Catalysts comprising molecular sieves
    • C07C2529/89Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Abstract

The invention discloses a strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method, which comprises 1-5 parts of strontium, 1-3 parts of tantalum and the balance of Ti-MWW molecular sieve according to 100 parts by weight; meanwhile, the invention also discloses a preparation method of the catalyst and application of the catalyst in preparation of 2-pentanone from ethanol by a liquid phase method. When the catalyst provided by the invention is used for preparing 2-pentanone, cheap coal-based ethanol is used as a raw material, so that the raw material cost is low; the strontium-tantalum-titanium trimetal oxide is used as a catalyst, raw material ethanol is used as a solvent, 2-pentanone is prepared in a slurry bed reactor in a high selectivity of liquid and solid phases, the conversion rate of the ethanol is more than 80%, and the selectivity of the product 2-pentanone is more than 70%.

Description

Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof
Technical Field
The invention belongs to the technical field of industrial catalysis, and particularly relates to a strontium-tantalum-titanium trimetallic oxide catalyst for preparing 2-pentanone from ethanol by a liquid phase method, and a preparation method and application thereof.
Background
Methyl propyl ketone (2-pentanone), also known as 2-pentanone, is a colorless liquid of chemical synthesis. The main application of the compound is to serve as an industrial solvent, and the compound can be widely used for manufacturing various oil-resistant gaskets, rubber tubes, airplane fuel tanks, flexible packages, printing and dyeing rubber rollers, cable materials, adhesives and the like, can also serve as an organic synthesis intermediate and a medical synthesis intermediate, and can be used for synthesizing vasodilator drugs Virga. 2-pentanone is also an excellent organic solvent, can be used as an excellent dewaxing agent of lubricating oil, a solvent of nitro spray paint and synthetic resin coating, can be used as an extracting agent and the like, and is an indispensable elastic material in the industries of automobiles, aviation, petroleum, copying and the like.
The 2-pentanone can be prepared by the ammoxidation of butene and can also be prepared by the catalysis of butanol and ammonia, and the traditional 2-pentanone synthesis method is the oxidative dehydrogenation of 2-pentanol or the co-heating of butyrylacetic acid ethyl ester and water. Chinese patents CN 1660749A and CN 1660750A disclose K-Pd/ZrO 2 Catalyst of/MnO/ZnO, which can be used for synthesizing 2-pentanone from ethanolHowever, the catalyst component in the process is complex and difficult to regulate and control; meanwhile, the use of noble metals and the catalytic reaction process need to be carried out under certain pressure, and the like. Chinese patent CN 106478386A discloses a new type of CeO 2 As a catalyst, the method for preparing 2-pentanone from ethanol has the problems of overhigh reaction temperature, low product selectivity and the like.
At present, various 2-pentanone production methods have the problems of serious three-waste pollution, low product selectivity, difficult product separation and purification and the like. If the 2-pentanone can be prepared by the ethanol liquid phase one-step method at low temperature and normal pressure with high selectivity, the production cost and equipment investment are greatly reduced, the process flow is simplified, and a green, environment-friendly and competitive production route is realized.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by using liquid phase ethanol and the preparation method thereof, and simultaneously provides the application of the catalyst in preparing 2-pentanone, so that the 2-pentanone can be prepared with high selectivity, the reaction condition is mild, and the cost is low.
The strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by using ethanol through a liquid phase method comprises, by weight, 100 parts of strontium 1-5 parts, 1-3 parts of tantalum and the balance of a Ti-MWW molecular sieve.
Preferably, the catalyst consists of 5 parts of strontium, 1 part of tantalum and 94 parts of Ti-MWW molecular sieve.
The Ti-MWW molecular sieve is prepared by adopting the prior art.
The preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method comprises the following steps:
(1) grinding the Ti-MWW molecular sieve for later use;
(2) at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine being 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine being 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
(3) adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 12-48h at room temperature, and then heating to 60-90 ℃ for secondary purification for 6-12 h;
(4) filtering, washing with distilled water of the same volume for 2-5 times, drying, roasting, and naturally cooling to obtain the catalyst.
Preferably, the drying conditions are drying at 110-140 ℃ for 4-6 h.
Preferably, the roasting condition is roasting at 500-550 ℃ for 4-12 h.
A method for preparing 2-pentanone from ethanol by a liquid phase method comprises the following specific steps: filling catalyst in a slurry bed reactor to form a catalyst bed layer, taking ethanol as a raw material, and reacting at the temperature of 50-60 ℃, under the normal pressure and at the weight space velocity of 0.1-1h -1 Introducing the mixed solution into the slurry bed reactor under the condition of (1), and rectifying the mixed solution to obtain 2-pentanone through the catalyst bed layer; the unreacted ethanol after rectification is circulated back to the slurry bed reactor;
wherein, the catalyst is the catalyst of the invention.
Preferably, the method for preparing 2-pentanone by using liquid phase ethanol comprises the following steps of filling a catalyst in a slurry bed reactor to form a catalyst bed layer, taking ethanol as a raw material, and reacting at 60 ℃ under normal pressure at a weight space velocity of 0.1h -1 Introducing the mixed solution into the slurry bed reactor under the condition of (1), and rectifying the mixed solution to obtain 2-pentanone through the catalyst bed layer; the unreacted ethanol after rectification is circulated back to the slurry bed reactor.
The invention has the advantages that:
(1) when the catalyst provided by the invention is used for preparing 2-pentanone, cheap coal-based ethanol is used as a raw material, so that the raw material cost is low; the strontium-tantalum-titanium trimetal oxide is used as a catalyst, raw material ethanol is used as a solvent, 2-pentanone is prepared in a slurry bed reactor in a high selectivity of liquid and solid phases, the conversion rate of the ethanol is more than 80%, and the selectivity of the product 2-pentanone is more than 70%;
(2) when the 2-pentanone is prepared, the raw materials have no toxicity, the preparation process has no three-waste discharge, and the environmental pollution is small;
(3) when 2-pentanone is prepared, ethanol is used as a raw material and a solvent, and simultaneously, because the trimetal oxide meets the effects of a molecular sieve and the solvent, the possibility of ethanol disproportionation to other products is reduced, the generation of byproducts is reduced, the catalytic reaction under normal pressure is realized, the reaction condition is mild, and the equipment investment and the operation cost are reduced; the selectivity of 2-pentanone is improved by utilizing the molecular sieve shape selection effect, the reaction product composition is simple, and the separation and purification process cost is low.
Detailed Description
Example 1
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol comprises 5 parts of strontium, 1 part of tantalum and 94 parts of Ti-MWW molecular sieve; the catalyst number is YCSY-01;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method comprises the following steps:
(1) grinding the Ti-MWW molecular sieve for later use;
(2) at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
(3) adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 24 hours at room temperature, and then heating to 80 ℃ for secondary purification for 8 hours;
(4) filtering, washing with distilled water of the same volume for 5 times, drying at 120 ℃ for 5h, roasting at 550 ℃ for 10h, and naturally cooling to obtain the catalyst.
Example 2
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol comprises 5 parts of strontium, 3 parts of tantalum and 92 parts of Ti-MWW molecular sieve; the catalyst is numbered YCSY-02;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method comprises the following steps:
(1) grinding the Ti-MWW molecular sieve for later use;
(2) at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
(3) adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 12h at room temperature, and then heating to 60 ℃ for secondary purification for 12 h;
(4) filtering, washing with distilled water of the same volume for 2 times, drying at 110 ℃ for 6 hours, roasting at 500 ℃ for 12 hours, and naturally cooling to obtain the catalyst.
Example 3
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method is composed of 2 parts of strontium, 1 part of tantalum and 97 parts of Ti-MWW molecular sieve; the catalyst is numbered YCSY-03;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method comprises the following steps:
(1) grinding the Ti-MWW molecular sieve for later use;
(2) at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
(3) adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 48 hours at room temperature, and then heating to 90 ℃ for secondary purification for 6 hours;
(4) filtering, washing with distilled water of the same volume for 5 times, drying at 140 ℃ for 4h, roasting at 550 ℃ for 4h, and naturally cooling to obtain the catalyst.
Example 4
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method is composed of 4 parts of strontium, 1 part of tantalum and 95 parts of Ti-MWW molecular sieve; the catalyst number is YCSY-04;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method comprises the following steps:
(1) grinding the Ti-MWW molecular sieve for later use;
(2) at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
(3) adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 36h at room temperature, and then heating to 75 ℃ for secondary purification for 9 h;
(4) filtering, washing with distilled water of the same volume for 4 times, drying at 120 ℃ for 5h, roasting at 500 ℃ for 8h, and naturally cooling to obtain the catalyst.
Example 5
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method is composed of 2 parts of strontium, 2 parts of tantalum and 96 parts of Ti-MWW molecular sieve; the catalyst number is YCSY-05;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through the liquid phase method is the same as that of example 4.
Example 6
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by using ethanol through a liquid phase method is composed of 2 parts of strontium, 3 parts of tantalum and 95 parts of Ti-MWW molecular sieve; the catalyst is numbered YCSY-06;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through the liquid phase method is the same as that of example 4.
Example 7
A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method is composed of 1 part of strontium, 1 part of tantalum and 98 parts of Ti-MWW molecular sieve; catalyst number YCSY-07;
the preparation method of the strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through the liquid phase method is the same as that of example 4.
Applications of
The catalyst prepared by the embodiment of the invention is applied to the liquid phase method for preparing 2-pentanone by ethanol, and the specific preparation method is as follows: the catalyst prepared by the embodiment of the invention is filled in a slurry bed reactor to form a catalyst bed layer, ethanol is used as a raw material, the reaction temperature is 50-60 ℃, the reaction pressure is normal pressure, and the weight space velocity is 0.1-1h -1 Introducing the mixed solution into the slurry bed reactor under the condition of (1), and rectifying the mixed solution to obtain 2-pentanone through the catalyst bed layer; the unreacted ethanol after rectification is circulated back to the slurry bed reactor; the catalytic performance of the catalyst was evaluated, and the specific reaction conditions and results are shown in table 1.
TABLE 1 reaction conditions and results
Figure 145443DEST_PATH_IMAGE001

Claims (7)

1. A strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by ethanol through a liquid phase method is characterized in that: the catalyst consists of 1-5 parts of strontium, 1-3 parts of tantalum and the balance of Ti-MWW molecular sieve according to 100 parts by weight;
the catalyst is prepared by the following method:
grinding the Ti-MWW molecular sieve for later use;
at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 12-48h at room temperature, and then heating to 60-90 ℃ for secondary purification for 6-12 h;
filtering, washing with distilled water of the same volume for 2-5 times, drying, roasting, and naturally cooling to obtain the catalyst.
2. The strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone from ethanol by the liquid phase method according to claim 1, wherein the strontium-tantalum-titanium trimetal oxide catalyst is characterized in that: the catalyst consists of 5 parts of strontium, 1 part of tantalum and 94 parts of Ti-MWW molecular sieve.
3. A process for preparing the catalyst of claim 1 or 2, characterized in that: the method comprises the following steps:
grinding the Ti-MWW molecular sieve for later use;
at the isoelectric point of taurine, adding strontium carbonate into an aqueous solution of taurine according to the molar ratio of strontium atoms to taurine of 1:1 to obtain a strontium carbonate-taurine mixed solution, and simultaneously adding tantalum carbonate into an aqueous solution of taurine according to the molar ratio of tantalum atoms to taurine of 1:1 to obtain a tantalum carbonate-taurine mixed solution; then mixing the strontium carbonate-taurine mixed solution with the tantalum carbonate-taurine mixed solution, and adjusting the pH of the mixed solution to taurine isoelectric point by using dilute hydrochloric acid to obtain an amino acid metal complex solution;
adding a ground Ti-MWW molecular sieve into the amino acid metal complex solution, soaking for 12-48h at room temperature, and then heating to 60-90 ℃ for secondary purification for 6-12 h;
filtering, washing with distilled water of the same volume for 2-5 times, drying, roasting, and naturally cooling to obtain the catalyst.
4. The method for preparing the catalyst according to claim 3, wherein: the drying condition is drying at 110-140 ℃ for 4-6 h.
5. The method for preparing the catalyst according to claim 4, wherein: the roasting condition is roasting for 4-12h at 500-550 ℃.
6. A method for preparing 2-pentanone from ethanol by a liquid phase method is characterized by comprising the following steps: the method comprises the following steps: filling a catalyst in a slurry bed reactor to form a catalyst bed layer, taking ethanol as a raw material, and reacting at the temperature of 50-60 ℃, the reaction pressure of normal pressure and the weight space velocity of 0.1-1h -1 Introducing the mixed solution into the slurry bed reactor under the condition of (1), and rectifying the mixed solution to obtain 2-pentanone through the catalyst bed layer;
wherein the catalyst is the catalyst of claim 1.
7. The method for preparing 2-pentanone from ethanol by using the liquid phase method according to claim 6, wherein the method comprises the following steps: the method comprises the following steps: filling a catalyst in a slurry bed reactor to form a catalyst bed layer, taking ethanol as a raw material, and reacting at the temperature of 60 ℃, the reaction pressure of normal pressure and the weight space velocity of 0.1h -1 Introducing the mixed solution into the slurry bed reactor under the condition of (1), and rectifying the mixed solution to obtain 2-pentanone through the catalyst bed layer.
CN202010680588.5A 2020-07-15 2020-07-15 Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof Active CN111790437B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010680588.5A CN111790437B (en) 2020-07-15 2020-07-15 Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010680588.5A CN111790437B (en) 2020-07-15 2020-07-15 Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof

Publications (2)

Publication Number Publication Date
CN111790437A CN111790437A (en) 2020-10-20
CN111790437B true CN111790437B (en) 2022-09-20

Family

ID=72807183

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010680588.5A Active CN111790437B (en) 2020-07-15 2020-07-15 Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN111790437B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113134387B (en) * 2021-04-28 2022-12-20 陕西延长石油(集团)有限责任公司 Inner framework metal high-silicon beta molecular sieve catalyst and preparation method and application thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102336734A (en) * 2010-07-15 2012-02-01 中国石油化工股份有限公司 Method for catalytic oxidation preparation of lactone from cycloalkane
WO2014035498A1 (en) * 2012-08-31 2014-03-06 Empire Technology Development Llc Lignin membranes and coatings
WO2016091058A1 (en) * 2014-12-11 2016-06-16 派尔科化工材料(启东)有限公司 Method for preparing 3-pentanone from 2-pentene
CN107250086A (en) * 2014-10-14 2017-10-13 吉沃公司 Ethanol is converted into the lower hydrocarbon of functionalization and the method for downstream hydrocarbon
CN109593033A (en) * 2017-09-30 2019-04-09 中国石油化工股份有限公司 A kind of method of oxidizing cyclohexanone
CN109803922A (en) * 2016-08-17 2019-05-24 沙特基础工业全球技术公司 For by nitrogen and hydrogen formed ammonia based on support type/graft type transition metal hydride heterogeneous catalyst/method
CN110872377A (en) * 2018-09-04 2020-03-10 中国科学院大连化学物理研究所 Metal cobalt complex polymer and preparation method and application thereof
CN111389457A (en) * 2020-04-22 2020-07-10 陕西延长石油(集团)有限责任公司 Catalyst and method for preparing methacrylic acid and propylene oxide by co-oxidation of isobutane and propylene

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7329354B2 (en) * 1998-06-09 2008-02-12 Ppt Technologies, Llc Purification of organic solvent fluids
CA2539666C (en) * 2005-03-24 2011-06-28 University Of Regina Catalysts for hydrogen production

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102336734A (en) * 2010-07-15 2012-02-01 中国石油化工股份有限公司 Method for catalytic oxidation preparation of lactone from cycloalkane
WO2014035498A1 (en) * 2012-08-31 2014-03-06 Empire Technology Development Llc Lignin membranes and coatings
CN107250086A (en) * 2014-10-14 2017-10-13 吉沃公司 Ethanol is converted into the lower hydrocarbon of functionalization and the method for downstream hydrocarbon
WO2016091058A1 (en) * 2014-12-11 2016-06-16 派尔科化工材料(启东)有限公司 Method for preparing 3-pentanone from 2-pentene
CN109803922A (en) * 2016-08-17 2019-05-24 沙特基础工业全球技术公司 For by nitrogen and hydrogen formed ammonia based on support type/graft type transition metal hydride heterogeneous catalyst/method
CN109593033A (en) * 2017-09-30 2019-04-09 中国石油化工股份有限公司 A kind of method of oxidizing cyclohexanone
CN110872377A (en) * 2018-09-04 2020-03-10 中国科学院大连化学物理研究所 Metal cobalt complex polymer and preparation method and application thereof
CN111389457A (en) * 2020-04-22 2020-07-10 陕西延长石油(集团)有限责任公司 Catalyst and method for preparing methacrylic acid and propylene oxide by co-oxidation of isobutane and propylene

Also Published As

Publication number Publication date
CN111790437A (en) 2020-10-20

Similar Documents

Publication Publication Date Title
CN101384542B (en) Process for the distillative separation of mixtures comprising monoethylene glycol and diethylentriamine
CN104232140A (en) Method for synthesizing high-density aviation fuel by using cyclopentanone as raw material
CN101805271B (en) Alicyclic diisocyanate and preparation method and purposes thereof
KR20120023728A (en) Method for producing aromatic amines
JP6242878B2 (en) Process for producing mono-N-alkyl-piperazine
CN111790437B (en) Strontium-tantalum-titanium trimetal oxide catalyst for preparing 2-pentanone by liquid phase method ethanol and preparation method and application thereof
CN104984751B (en) A kind of metal oxide catalyst and preparation method thereof
CN113231069B (en) Maleic anhydride bulk hydrogenation succinic anhydride preparation composite efficient catalyst and preparation method thereof
CN109821572B (en) Porous microsphere polymer supported metal type catalyst and preparation method and application thereof
CN108772074B (en) Catalyst for preparing diethylenetriamine by hydrogenation of ethylenediamine and preparation method thereof
CN104230741A (en) Synthetic method of octadecyl erucyl amide
CN104387340A (en) Method for preparing N-methyl piperazine and catalyst of N-methyl piperazine
CN108273507B (en) Method for reducing nitrile compound by catalytic hydrogenation
CN1312109C (en) Process for producing benzenedimethanmmine
CN109678734B (en) Method for preparing 2-methoxy ethylamine by directly catalyzing and aminating ethylene glycol monomethyl ether
EP3983374A1 (en) Products obtained by the conversion of glycolaldehyde derivatives and aminating agents and their conversion to ethyleneamines and ethanolamines
CN101579639A (en) Catalyst for synthesizing fatty nitrile, preparation method and applications
US7507863B2 (en) Process for producing nitrogen-containing compounds
US5648538A (en) Process for preparing diarylamines from arylamines
CN113398932B (en) Preparation method for preparing diamine by hydrogenation of dinitrile
CN111036268B (en) Alumina composite material, preparation method and application thereof, and synthetic method of n-valeronitrile
US9695121B2 (en) 2,6-bis-(aminomethyl)piperidine derivatives
CA1123012A (en) Selective hydrogenation of nitroaromatic acetylenes over an unsupported rus.sub.2 catalyst
CN111744546B (en) Copper-bismuth-titanium trimetal oxide catalyst for preparing N-ethylethylenediamine by liquid phase method ethanol, and preparation method and application thereof
WO2020249428A1 (en) Products obtained by the conversion of glycolaldehyde derivatives and aminating agents and their conversion to ethyleneamines and ethanolamines

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant